Layered double hydroxides supported nanopalladium catalysts for Heck-, Suzuki, Sonogashira-, and Stille type coupling reactions of haloarenes

Abstract

The present invention relates to a novel process for the preparation of a reusable heterogeneous nanopalladium (0) catalysts, which is a eco-friendly and economical process employing re-usable heterogeneous catalyst in place of soluble palladium catalysts for preparing coupling products by C—C bond formation reaction of haloarenes that include unreactive chloroarenes in the presence of base. The use of heterogeneous nanopalladium catalyst precludes the presence of palladium in traces with the product.

Description

[0001] The present invention relates to a process for the preparation of a reusable heterogeneous nanopalladium(0) catalysts on the solid support to perform C—C bond formation reactions such as Heck, Suzuki, Sonagashira, and Stille type reactions of haloarenes that include unreactive chloroarenes. Layered double hydroxides and Merrifield resin supported nanopalladium catalysts are prepared by an exchange of PdCl42− followed by reduction and well characterized for the first time.

[0002] This invention particularly relates to an ceo-friendly process employing re-usable heterogeneous catalyst in place of soluble palladium catalysts for preparing coupling products by C—C bond formation reaction of haloarenes that include unreactive chloroarenes in the presence of base. The ligand force heterogeneous layered double hydroxides supported nanopalladium (LDH-Pd0) catalyst using the basic LDH in place of basic ligands indeed exhibits higher activity and selectivity in the C—C coupling reactions of haloarenes that include electron poor and electron rich chloroarenes in nonaqueous ionic liquids (NAIL) over the homogeneous PdCl2 system. The coupling products find good applications as intermediates in the preparation of materials, natural products, and bioactive compounds.

[0003] There are serious disadvantages in performing the catalytic C—C bond formation reaction with iodoarenes and bromoarenes in the manufacture of olefins due to high cost of the starting materials. Despite the synthetic elegance and high turnover number, these coupling reactions suffer from serious limitations of using the expensive bromo and iodoarenes that precluded the wide use in industry. By employing the heterogeneous catalytic system and chloroarenes as starting materials, the cost naturally comes down due to easy recovery of the catalyst and low cost of chloroarenes when compared with bromo and iodoarenes.

[0004] References may he made to the publications, Organometallics 1992, 11, 1995, Angew. Chem. Int. Ed. 1998, 37, 481, J. Organomet. Chem. 1998, 572, 93, Angew. Chem. Int. Ed. Engl. 1995, 34, 2371, J Organomet. Chem. 1999, 576, 23 wherein Heck-olefination of chloroarenes is carried by palladium complexes under homogeneous conditions. The inherent disadvantages are difficulty in the recovery of palladium and usage of activated electron poor and nonactivated electron neutral chloroarenes.

[0005] References may be made to the publications Organometallics 1993, 12, 4734, J. Org. Chem. 1999, 64, 10, J. Am. Chem. Soc, 2001, 123,6989, Synlett, 2000, 11, 1589, J. Am. Chem. Soc. 1999, 121, 2123 wherein olefins are prepared from deactivated highly electron rich chloroarenes by palladium complexes. The inherent disadvantage is the usage of expensive sterically hindered phosphine palladium complexes.

[0006] Reference may be made to the publication Chem. Ear. J. 2000, 6, 1017 wherein Heck-olefination of deactivated highly electron rich chloroarenes is carried by palladacycle catalysts in the presence of nonaqucous liquids. The inherent disadvantages are the usage of additives and low yields.

[0007] Reference may be made to European patent DE-A 197 12 388.0,1997 wherein Heck-olefination of chloroarenes is carried by palladacycle catalyst using an additive. The inherent disadvantage is that no reaction occurs in the absence of phosphonium salt.

[0008] Reference may be made to the publications J. Am. Chem. Soc., 1998, 120, 9722 and Angew. Chem. Int. Ed, Engl., 1998, 37, 3387 wherein biphenyls are prepared using arylchlorides with palladium catalysts. The inherent disadvantage is the usage of expensive, air-sensitive phosphine ligands.

[0009] Reference may be made to a publication J. Organometallic Chem., 1998, 557, 93 wherein biphenyls are prepared using carbene ancillary ligands with aryl bromides and activated aryl chlorides with palladium catalyst. The drawbacks are longer reaction times and yield from the aryl chloride was relatively low.

[0010] Reference may be made to a publication J. Organomet. Chem. 2001, 634, 39 wherein diarylacetylenes are prepared using heterogeneous polymer anchored bis(pyrimidine)-based palladium catalyst with chlorobenzene with impressive turnover frequency. The drawback is that it was not tried for electron rich chloroarenes.

[0011] Reference may be made to the publication Synlett, 2000, 1043 wherein arylstannanes were prepared using palladium catalyst in the presence of potassium acetate. The drawback is that the usage of aryl iodides as substrates.

[0012] Objects of the Invention

[0013] The main object of the present invention, is a process for the preparation of a ligand free reusable heterogeneous nanopalladium(0) catalysts by an exchange of PdCl42− followed by reduction on the support selected from LDH and S′—NR3X wherein S′ is a unmodified surface support selected from resin and silica, R is an alkyl group selected from the group consisting of methyl, ethyl, propyl, butyl , X is selected from the group consisting of Cl, Br, I, F, OH. and OAc to perform C—C bond coupling reactions such as Heck, Suzuki, Sonagashira, and Stille type reactions with haloarenes that include unreactive chloroarenes under standard thermal and microwave conditions using solvents selected from nonaqueous ionic liquid, THF, dioxane, water, NMP at temperature ranging between 20 to 150° C. for a period ranging from 0.5 to 48 h under nitrogen atmosphere and obtaining the desired product by conventional method which obviates the drawbacks as detailed above.

[0014] Another object of the present invention is LDH as synthesised having interstitial anions such as chloride, nitrate. carbonate, sulfate or calcination of LDH having the said interstitial anions at temperatures in the range of 350 to 550 C are used as precursors for the preparation of LDH-Pd(0) catalysts.

[0015] Another object of the present invention is to reduce the reaction time by employing microwave irradiation. Using microwave irradiation, the rate of C—C coupling reaction is accelerated manifold with the highest turnover frequency ever recorded both in the case of electron poor and electron rich chloroarenes.

[0016] Still another object of the present invention is the quantity of nanopalladium catalyst used in the reaction is 0.1 to 3 mol % of palladium with respect to the substrate.

[0017] Yet another object of the present invention is to recover the heterogeneous palladium catalyst used in the C—C coupling reactions such as Heck, Suzuki, Sonagashira, and Stille type reactions by simple filtration and reuse for number of cycles with consistent activity.

SUMMARY OF THE INVENTION

[0018] The novelty of the present invention, is a process for the preparation of a ligand free reusable heterogeneous nanopalladium(0) catalysts by an exchange of PdCL42− followed by reduction on the support selected from LDH and S′—NR3X wherein S′ is a unmodified surface support selected from resin and silica, R is an alkyl group selected from the group consisting of methyl, ethyl, propyl, butyl, X is selected front the group consisting of Cl, Br, I, F, OH and OAc to perform C—C bond coupling reactions such as Heck, Suzuki, Sonagashira, and Stille type reactions with haloarenes that include unreactive chloroarenes under standard thermal and microwave conditions using solvents selected from nonaqucous ionic liquid, THF, dioxane, water, NMP at temperature ranging between 20 to 150° C. for a period ranging from 0.5 to 48 h under nitrogen atmosphere and obtaining the desired product by conventional method.

[0019] In an embodiment of the present invention, the quantity of nanopalladium(0) catalyst used in the reaction is 0.1 to 3 mol % of palladium with respect to the substrate.

[0020] In an embodiment of the present invention, nanopalladium (0) catalysts are recovered by simple filtration and reused for several cycles with consistent activity.

[0021] In another embodiment of the present invention, the solvents selected for the C—C bond formation reactions are nonaqueous liquid, water, 1,4-dioxane, THF, NMP.

[0022] In yet another embodiment of the present invention, the base used is selected from the known group consisting of triethylamine, tributylamine, potassium fluoride, potassium acetate.

[0023] In still another embodiment of the present invention, the reactions are preferably, effected at a known temperature in the range of 20 to 150° C. for a period 0.5 to 48 h.

[0024] In still another embodiment of the present invention, is to reduce the reaction time by employing microwave irradiation. Using microwave irradiation, the rate of C—C coupling reaction is accelerated manifold with the highest turnover frequency ever recorded both in the case of electron poor and electron rich chloroarenes.

[0025] In yet another embodiment of the present invention, a phosphine free new recyclable heterogeneous catalytic system. was developed to dispense the use of expensive and air sensitive basic phosphincs for palladium catalyzed coupling reactions of chloroarenes. The basic support, Mg—Al layered double hydroxides (LDH) selected not only stabilizes the nanopalladium particles but also provides the adequate electron density to the anchored Pd0 species to facilitate oxidative addition of even the deactivated electron rich chloroarenes.

DETAILED DESCRIPTION OF THE INVENTION:

[0026] Heterogeneous nanopalladium(0) catalysts are prepared by an exchange of PdCl42− on the support selected from LDH and S′—NR3X wherein S′ is a unmodified surface support selected from resin and silica, R is an alkyl group selected from the group consisting of methyl, ethyl, propyl, butyl, X is selected from the group consisting of Cl, Br, I, F, OH and OAc in an aqueous solvent at a temperature ranging between 20 to 30° C. for a period ranging from 5 to 24 h under nitrogen atmosphere followed by filtration and reduction with hydrazine hydrate in ethanol at room temperature. Filtration gave the desired nanopalladium(0) catalysts.

[0027] C—C bond coupling products are prepared by using the recyclable nanopalladium(0) catalysts by Heck, Suzuki, Sonagashira, and Stille type reactions of haloarenes that include unreactive chloroarenes in a under standard thermal and microwave conditions using solvents selected from nonaqueous ionic liquid, water, THF, dioxan, and NMP at a temperature ranging between 20 to 150° C. for a period 0.5 to 48 h under nitrogen atmosphere, and obtaining the pure C—C coupling products by a conventional method.

[0028] The palladium content in the catalyst ranges between 0.1 to 3 mol % with respect to the substrate. Nanopalladium (0) catalysts are recovered by simple filtration and reused for several cycles with consistent activity.

[0029] The solvents selected for the C—C bond formation reaction is selected from the group consisting of nonaqueous ionic liquid, water, 1,4-dioxane, THF, NMP or any mixture thereof The base used is selected from the group consisting of triethylamine, tributylamine, potassium fluoride, potassium acetate.

[0030] Scientific Explanation:

[0031] In the present invention, we synthesized LDH, silica, resin supported nanopalladium catalysts for the first time and used in catalytic amounts for preparing coupling products by C—C bond formation reactions involving Heck-, Suzuki-, Sonagashira- and Stille type coupling of haloarenes that include chloroarenes in presence of base.

[0032] Heterogeneous nanopalladium(0) catalysts are prepared by an exchange of PdCl42− followed by reduction on silica or resin or LDH.

[0033] The nanopalladium (0) on supports is responsible for the activity of catalyst in C—C coupling reactions. The activity of heterogeneous nanopalladium catalysts is similar or higher than the homogeneous counter parts. The basic support, Mg—Al layered double hydroxides (LDH) is selected as the material of choice, which not only stabilizes the nanopalladium particles but also provides the adequate electron density to the anchored Pd0 species to facilitate oxidative addition of even the deactivated electron rich chloroarenes.

[0034] Higher yields and stereoselectivities are obtained when nanopalladium catalysts are used. Incidentally this forms the first report of heterogeneous palladium catalyst employed in the Stille type coupling. The consistent activity obtained for several cycles makes the process economical and possible for commercial realization.

[0035] The coupling products find good applications as intermediates in the preparation of materials, natural products, and bioactive compounds. Thus this invention offers the best techno-economic route for the synthesis of coupling products. Therefore, nanopalladium catalysts are better option for the C—C bond formation reaction of haloarenes that include chloroarenes.

[0036] Nanopalladium catalysts are prepared as exemplified and used in catalytic amounts for preparing coupling products by C—C bond formation reaction in presence of base in a heterogeneous way as described in the examples.

[0037] The following examples are given by way of illustration of the present invention and therefore should not be construed to limit the scope of the invention.

[0038] Preparation of Nanopalladium Catalysts

EXAMPLE 1

[0039] Preparation of LDH (Mg—Al—Cl) (1)

[0040] A mixture of MgCl2.6H2O (30.49 g, 0.15 mmol) and AlCl3.6H2O (12.07 g, 0.05 mmol) was dissolved in 200 ml of deionised water. To this aqueous solution, 100 ml of NaOH (2M) solution was slowly added at 25° C. and a further amount of 2M NaOH solution was added to maintain a pH of 10 under nitrogen flow. The resulting suspension was stirred overnight at 70° C. The solid product was isolated by filtration, washed thoroughly with deionised water and dried overnight at 80° C. All the synthetic steps were carried out using decarbonated water.

EXAMPLE 2

[0041] Preparation of Na2PdCl4 (2)

[0042] Na2PdCl4 was prepared by refluxing PdCl2 (1.77 g, 10 mmol) and sodium chloride (0.58 g, 10 mmol) in 50 mL for 4 h. The solution was filtered in hot condition to avoid NaCl contamination. Evaporation of the filtrate gave dark brown flakes (2.88 g, 98%).

EXAMPLE 3

[0043] Preparation of LDH-PdCl4 (3)

[0044] Mg—Al—Cl (1.5 g) was suspended in 150 mL of aqueous Na2PdCI4 (0.441 g, 1.5 mmol) solution and stirred at 25° C. for 12 h under nitrogen atmosphere. The solid catalyst was filtered, washed thoroughly with 500 mL of water and vacuum-dried to obtain 1.752 g of LDH-PdCl4 (0.86 mmol of Pd per gram).

EXAMPLE 4

[0045] Preparation of LDH-Pd0 (4)

[0046] LDH-PdCl4 (1 g) was reduced with hydrazine hydrate (1 g, 20 mmol) in ethanol (10 mL) for 3 h at room temperature, filtered and washed with ethanol to give an air stable black powder (0.95 mmol of Pd per gram).

EXAMPLE 5

[0047] Preparation of Resin-PdCl4 (5)

[0048] Resin was obtained by quaternization of triethylamine (2.1 mL, 21 mmol) with one gram of chloromethylated styrene-divinylbenzene copolymer (Merrifield resin, capacity ˜2.1 mcquiv/g) in chloroform (20 mL) under reflux for 24 h. Quaternary ammonium resin (1 g) was suspended in 100 mL of (0.294 g, 1 mmol) aqueous Na2PdCl4 solution and stirred at 25° C. for 12 h under nitrogen atmosphere. The solid catalyst was filtered, washed thoroughly with water (300 mL) and vacuum-dried to obtain resin-PdCl4 (0.8 mmol of Pd per gram).

EXAMPLE 6

[0049] Preparation of Resin-Pd0 (6)

[0050] Resin-PdCl4 (1 g) was reduced with hydrazine hydrate (1 g, 20 mmol) in ethanol (10 mL) for 3 h at room temperature, filtered and washed with ethanol to give an air stable black bcads (0.87 mmol of Pd per gram).

EXAMPLE 7

[0051] Preparation of Silica-PdCl4 (7)

[0052] Modified silica was obtained by quaternization of triethylamine (0.7 mL, 7 mmol) with bromopropylsilica (capacity 0.7 mcquiv/g) in chloroform (20 mL) under reflux for 24 h. 1 g of quaternary ammonium silica was suspended in 100 mL of 0.33 mmol aqueous Na2PdCl4 solution and stirred at 25° C. for 12 h under nitrogen atmosphere. The solid catalyst was filtered, washed thoroughly with 300 mL of water and vacuum dried to obtain SiO2—PdCl4.

EXAMPLE 8

[0053] Preparation of Silica-Pd0 (8)

[0054] Silica-PdCl4 (1 g) was reduced with hydrazine hydrate (1 g, 20 mmol) in ethanol (10 mL) for 3 h at room temperature, filtered and washed with ethanol to give an air stable black powder.

C—C Bond Forming Reactions

[0055] The C—C bond forming reactions were performed using LDH-Pd0 catalysts to evaluate nanopalladium catalysts of the present invention.

[0056] 1. Heck-Olefination. 1

EXAMPLE 9

[0057] Heck-Olefination between Chlorobenzene and Styrene Catalysed by LDH-Pd0 under Thermal Conditions

[0058] In a 100 mL Schlenk flask, the NAIL (3.23 g, 10 mmol)(NBu4Br) was heated to melt (130° C.) and degassed with nitrogen and vacuum prior to the addition of other reagents. After cooling the NAIL to room temperature, LDH-Pd0 (3 mol %), tri-n-butyl amine (222 mg, 1.2 mmol) were added. The styrene (1.2 mmol) and chlorobenzene (1 mmol) were then added and the reaction was heated to 130° C. and stirred for 10-40 h under nitrogen atmosphere, After completion of the reaction, the LDH-Pd0 catalyst was filtered and washed with water and dichloromethane. After removing the solvent, the crude material was chromatographed on silica gel or recrystallized from ethanol to afford the trans-stilbene.

EXAMPLE 10-17

[0059] The procedure was followed as in example 9 with various substrates under thermal conditions and the results are presented in Table 1.

TABLE 1
LDH-Pd0 Catalyzed Heck-Olefination of Chloroarenes under thermal
conditionsa
Example	Chloroarene	Olefin	Time (h)	Yield (%)
9	2	3	30	98
10	4	5	10	95
11	6	7	15	97
12	8	9	15	98
13	10	11	15	93
14	12	13	40	86
15	14	15	40	76 (5)b
16	16	17	30	96 (55)b
17	18	19	30	92 (51)b
aChloroarene (1 mmol), olefin (1.2 mmol) LDH-Pd0 (3 mol %), [NBu4]Br (10 mmol), and tri-n-butyl amine (1.2 mmol). Reactions are conducted at 130° C.
bThe values in parentheses refer to the homogeneous reaction conducted with PdCl2 under identical conditions.

EXAMPLE 18

[0060] Heck-Olefination between Chlorobenzene and Styrene Catalysed by LDH-Pd0 under Microwave Conditions.

[0061] Styrene (1.2 mmol), chlorobenzene (1 mmol), LDH-Pd0 (3 mol %), tri-n-butyl amine (222mg, 1.2 mmol) and NAIL (3.23 g, 10 mmol) were taken in a teflon vessel, closed and irradiated in a Miele Electronic M270 microwave oven at 400 W and 130° C. for 0.5-1 h. After completion of the reaction, the LDH-Pd0 catalyst was filtered and washed with water and dichloromethane. After removing the solvent, the crude material was chromatographed on silica gel to afford the trans-stilbene.

EXAMPLE 19-26

[0062] The procedure was followed as in example 18 with various substrates under microwave conditions and the results are presented in Table 2.

TABLE 2
LDH-Pd0 Catalyzcd Heck-Olefination of Chloroarenes under microwave
conditionsa
Example	Chloroarene	Olefin	Time (h)	Yield (%)
18	20	21	0.5	95
19	22	23	0.5	96
20	24	25	0.5	93
21	26	27	0.5	95
22	28	29	0.5	91
23	30	31	1	85
24	32	33	1	80
25	34	35	0.5	92
26	36	37	0.5	90
aChloroarene (1 mmol), olefin (1.2 mmol) LDH-Pd0 (3 mol %), [NBu4]Br (10 mmol), and tri-n-butyl amine (1.2 mmol). Microwave power 400 W and temperature 130° C.

EXAMPLE 27-32

[0063] In an effort to compare the reactivity of LDH-Pd0 with other heterogeneous catalysts namely Pd/C, Pd/SiO2, resin-Pd0 and Pd/Al2O3 in the Heck-olefination, separate experiments were conducted under identical conditions with the same ingredients and the results are summarized in Table 3. The activity of various catalysts in the Heck-olefination olefination of 4chloroanisole is found to be in the order: LDH-Pd°>resin-Pd0>Pd/Al2O3>Pd/SiO2. These results indicate that the basic support, LDH facilitates the oxidative addition of Pd0 with 4-chloroanisole and eventually the Heck-olefination reaction.

[0064] The procedure was followed as in example 9 with various catalysts between 4-chloroanisole and styrene under thermal conditions and the results are presented in Table 3.

TABLE 3
Heck-Olefination of 4-Chloroanisole with Styrene Using Various
Palladium Catalystsa
Example	Catalyst	Yield (%)
27	LDH-Pd0	76
28	resin-Pd0	29
29	Pd/C	28
30	Pd/Al2O3	22
31	Pd/SiO2	15
32	PdCl2	5
a4-chloroanisole (1 mmol), olefin (1.2 mmol), Palladium catalyst (3 mol %), [NBu4]Br 3.23 g (10 mmol), and tributylamine (1.2 mmol) were stirred at 130° C. for 40 h.

[0065] 2. Suzuki Coupling 38

EXAMPLE 33

[0066] Suzuki Coupling between Chlorobenzene and Phenylboronic Acid Catalysed by LDH-Pd0

[0067] Chlorobenzene (1 mmol), phenylboronic acid (1.5 mmol), potassium fluoride (3 mmol), LDH-Pd0 (1 mol %) and 1,4-dioxane-water (5:1, 5 mL) were charged in a round-bottomed flask. Reactions were carried out at 100° C. for 10 h. After completion of the reaction (monitored by TLC), the catalyst was filtered and the reaction mixture was poured into water and the aqueous phase was extracted with ether. After drying, the corresponding product was purified by crystallization from diethyl ether-pentane.

EXAMPLES 34-40

[0068] The procedure was followed as in example 33 and the results are given in Table 4.

TABLE 4
Suzuki Coupling Reactions of Chloroarenes with Arylboronic
Acidsa
Example	Arylboronic acid	Haloarene	Yield (%)
33	39	40	93 (92)b
34	41	42	90
35	43	44	60
36	45	46	80
37	47	48	70
38	49	50	60
39	51	52	90
40	53	54	88
aChloroarene (1 mmol), arylboronic acid (1.5 mmol), LDH-Pd0 (1 mol %) and KF (3 mmol), 100° C., 10 h. All the reactions were carried out with 1,4-dioxane-water (5:1, 5 mL) as solvent.
bUnder NAIL conditions, 8 h.

[0069] 3. Sonogashira Coupling 55

EXAMPLE 41

[0070] Sonagashira Coupling between Chlorobenzene and Phenylacetylene Catalysed by LDH-Pd0

[0071] To a stirred slurry of chlorobenzene (1 mmol), cuprous iodide (7.6 mg, 0.04 mmol), and LDH-Pd0 (1 mol %), in THF (2 mL) and water (4 mL) was added triethylamine (152 mg, 1.5 mmol). A solution of 1 .25 mmol of phenylethylene in THF (2 mL) was then added over 2 h. After completion of the reaction, the solvent was evaporated, and the residue was treated with pentane. The solution was filtered to obtain the catalyst and evaporation of the solvent gives the coupling product.

EXAMPLES 42-43

[0072] The procedure was followed as in example 41 and the results are given in Table 5.

TABLE 5
Cross Coupling Reactions Between Phenylacetylene and Chloroarenesa
Example	Chloroarene	Phenylacetylene	Time (h)	Yields (%)
41	56	57	30 27	95 95b
42	58	59	48	60
43	60	61	40	82
aChloroarene (1 mmol), phenylacetylene (1.1 mmol), LDH-Pd0 (1 mol %), Et3N (1.5 mol), 80° C. All reactions were carried out with THF-water (1:1, 8 mL) as solvent system.
bUnder NAIL conditions.

[0073] 4. Stille Type Coupling 62

EXAMPLE 44

[0074] Stille Type Couping between Chlorobenzene and Tributyltin Reagent Catalysed by LDH-Pd0

[0075] A round-bottomed flask was charged with LDH-Pd0 (1 mol %), potassium acetate (294 mg, 3 mmol), and NMP (4 ml). To this 4-chloroanisole (1 mmol) and tributyltin hydride (2 mmol) were added successively, and the mixture was stirred at 50° C. for 16 h.

[0076] The reaction mixture was diluted with benzene, washed with water and catalyst was collected for next cycle.

EXAMPLES 45-49

[0077] The procedure was followed as in example 44 and the results are given in Table 6.

TABLE 6
Stannylation of Haloarenes with LDH-Pd0 catalysta
Example	Chloroarene	Tin reagent	Yield
44	63	Bu3Sn—H	90 (91)b
45	64	Bu3Sn—H	80
46	65	Bu3Sn—H	90
47	66	67	80
48	68	69	65
49	70	71	70
aChloroarene (1 mmol), trialkyltin reagent (2 mmol), potassium acetate (3 mmol), LDH-Pd0 (2 mol %). All the reactions were carried out with NMP as solvent, 50° C., 16 h.
bUnder NAIL conditions, 12 h.

[0078] The main advantages of the present invention are:

[0079] 1. A novel and ecofriendly process for the synthesis of coupling products from haloarenes that include highly unreactive chloroarenes by C—C bond formation is presented.

[0080] 2. The present process dispenses the use of soluble palladium catalysts instead a heterogeneous reusable LDH-Pd(0) is used.

[0081] 3. Nanopalladium catalyst, LDH-Pd(0) is prepared and used as heterogeneous catalyst for the synthesis of coupling products by C—C bond formation reactions. The use of heterogeneous nanopalladium catalyst precludes the presence of palladium in traces with the product.

[0082] 4. The stereoselectivity and the yields are good.

[0083] 5. The work-up procedure is simple.

[0084] 6. The catalyst is subjected to many recycles, which displayed consistent activity.

[0085] 7. The present process is environmentally safe since there is no disposal problem.

[0086] 8. The process is economical.

Claims

1. A process for the preparation of a ligand free reusable heterogeneous nanopalladium(0) catalyst obtained by an exchange of PdCl42− followed by reduction on the support selected from LDH and S′—NR3X wherein S′ is a unmodified surface support selected from resin and silica, R is an alkyl group selected from the group consisting of methyl, ethyl, propyl, butyl, X is selected from the group consisting of Cl, Br, I, F, OH and OAc to perform C—C bond coupling reactions such as Heck, Suzuki, Sonagashira, and Stille type reactions with haloarenes that include unreactive chloroarenes under standard thermal and microwave conditions using solvents selected from nonaqueous ionic liquid, THF, dioxane, water, NMP at temperature ranging between 20 to 150° C. for a period ranging from 0.5 to 48 h under nitrogen atmosphere and obtaining the desired product by conventional method.

2. A process as claimed in claim 1, wherein the LDH-Pd0 useful as a catalyst, of the formula [M(II)1-xM(III)x (OH)2] [Pd(0)] wherein LDH is a class of layered material consisting of alternating cationic M(II)1-xM(III)x (OH)2x+ and anionic An−.zH2O layers, MII is a divalent cation selected from the group consisting of Mg2+, Mn2+, Fe2+, Co2+, Ni2+, Cu2+, Zn2+ and Ca2+ and MIII is a trivalent ion selected from the group consisting of Al3+, Cr3+, Mn3+, Fe3+ and Co3+, An− is an interstitial anion selected from nitrate, carbonate and chloride, x is the mole fraction having integral value ranging from 0.2 to 0.33, and z is the number of water molecules and ranges from 1 to 4.

3. A process as claimed in claims 1-2, wherein the said process for the preparation of the catalyst LDH-Pd0 of the formula [M(II)1-xM(III)x (OH)2] [Pd(0)] comprises reacting sodium palladate of formula Na2PdCl4 with a LDH of formula [M(II)1-xM(III)x (OH)2x+] [An−] wherein MII is a divalent cation selected from the group consisting Mg2+, Mn2+, Fe2+, Co2+, Ni2+, Cu2+, Zn2+ and Ca2+ and MIII is a trivalent ion selected from the group consisting Al3+, Cr3+, Mn3+, Fe3+ and Co3+, and An− is an interstitial anion selected from nitrate, carbonate and chloride, x is the mole fraction having integral value ranging from 0.2 to 0.33, and z is the number of water molecules and ranges from 1 to 4 in an aqueous solvent at a temperature ranging between 20 to 30° C. for a period of 5 to 24 h under the nitrogen atmosphere followed by reduction, filtration and washing to obtain the desired catalyst.

4. A process as claimed in claims 1-3, wherein the palladium content in the catalyst ranges between 0.1 to 3 mol % with respect to the substrate.

5. A process as claimed in claims 1-4, wherein nanopalladium (0) catalysts are recovered by simple filtration and reused for several cycles with consistent activity.

6. A process as claimed in claims 1-5, wherein the solvents for the C—C bond formation reaction are selected from the group consisting of nonaqueous ionic liquid, water, dioxane, THF, NMP or any mixture thereof.

7. A process as claimed in claims 1-6, wherein the base used is selected from the group consisting of triethylamine, tributylamine, potassium fluoride, potassium acetate and obtaining the desired product by conventional method.

8. A process as claimed in claims 1-7, wherein a phosphine free new recyclable heterogeneous catalytic system was developed to dispense the use of expensive and air sensitive basic phosphines for palladium catalyzed coupling reactions of chloroarenes.